Process and system for separation and recovery of perfluorocompound gases
Abstract
Processes and systems to recover at least one perfluorocompound gas from a gas mixture are provided. In one embodiment the inventive process comprises the steps of a) providing a gas mixture comprising at least one perfluorocompound gas and at least one carrier gas, the gas mixture being at a predetermined pressure; b) providing at least one glassy polymer membrane having a feed side and a permeate side; c) contacting the feed side of the at least one membrane with the gas mixture; d) withdrawing from the feed side of the membrane as a non-permeate stream at a pressure which is substantially equal to the predetermined pressure a concentrated gas mixture comprising essentially the at least one perfluorocompound gas; and e) withdrawing from the permeate side of the membrane as a permeate stream a depleted gas mixture comprising essentially the at least one carrier gas.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1. A process for the separation of perfluorocompound gases from a gas mixture, said process comprising the step of:
contacting a gas mixture comprising at least one carrier gas and at least one perfluorocompound gas selected from the group consisting of CF 4 , C 2 F 6 , C 3 F 8 , C 4 F 10 , and NF 3 with a membrane which permeates said at least one carrier gas faster than said at least one perfluorocompound gas.
2. The process according to claim 1 , wherein said at least one carrier gas is air, nitrogen, oxygen, argon, helium, or mixtures thereof.
3. The process according to claim 1 , wherein said membrane is a glassy polymeric membrane.
4. The process according to claim 1 , wherein said at least one perfluorocompound gas is CF 4 .
5. The process according to claim 1 , wherein said at least one perfluorocompound gas is C 2 F 6 .
6. The process according to claim 1 , wherein said at least one perfluorocompound gas is C 3 F 8 .
7. The process according to claim 1 , wherein said at least one perfluorocompound gas is C 4 F 10 .
8. The process according to claim 1 , wherein said at least one perfluorocompound gas is NF 3 .Cited by (0)
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